Process of dehydrating animal and vegetable substances.



' E. W. COOKE. PROCESS OF DEHAYDRATINGANIML AND VEGETABLE SUBSTANGES.

APPLICATION FILED JAN. 30, 1905.

N UNITED sTATEs PATENT OFFICE.

ERNEST WILLIAM coOKE OE NEW YORK, N. Y., AssIGNoIa BY' MEsNE ASSIGNMENTS,

` 'To THE coxEI. OOMPANY,A CORPORATION OE NEW JERSEY.

PROCESS OF DEHYDRATING ANIMAL AND VEGETABLE SUBSTANCES.

Specicatio'n of Letters Patent.

Patented May 7, 1912.

Application tiled J'anuarylSO, *1905. Serial No.243,304f

To all whom 'it may concern:

Be it known that I, ERNEST W'. COOKE, a citizen of the United States, residing at New York, in the county of New York and State of New York, have invented certain new and useful Improvements in the Process of Dehydrating Animal and Vegetable Substances; and I do declare the following to be a full, clear, and exact description of the invention, such asiwill enable others skilled.

in theart to which it appertains to make and use the same, reference being had to the y accompanying drawings, and to the let-ters and' figures of reference marked thereon, which form a part of this specification.

My invention consists in a process of dehydrating succulent animal and vegetable food substances by means of which I have obtained results which I believe to have never been before'obtained, in that I am enabled, by the operation'of my process, to

remove all, or the larger part. of the water contained in the material treated without injuring the texture or cellular structure of the animal or vegetable products, however delicate it may be. A

The materials treated 4by 'my process can be perfectly restored to their original, undehydrated condition by the simple addition'and vabsorption of water, either hot or cold.

My process is more particularly-applicalble to the dehydration of succulent food substances, which are .thereby greatlylreduced in weight and bulk, thus immensely facilitating their transportatiOnand storage, and are thereafter available at any time for restoration to edible condition by thefsimple addition of water, which restores 'them so perfectly that .they cannot-be distinguished from the fresh products. l

Itis well known that it is practically im'- possible to obt-ain fresh vegetables, fruit,

l etc., at all seasons, even in tropical climates,

and indeed in many partsof the earth, it is practically impossibleto obtain such at any time. The absence of fresh -food substances is often not only a hardship, but is the cause of serious suffering and sickness. The practice of my invention therefore will be of the greatest benefit -to large numbers of the human race, permitting as it does, the

easy transportation and storage, and the keeping for an unlimited time, of all Varieties of dehydrated vegetables, aswell as fruit and animal food substances, which require not-hing but` water to restore them absolutely to the condition of freshness in which they were when originally treated by my process.

.My inventionnust not be confused with methods heretofore. employed for preserving vegetablespetc., in which preservatives are invariably used,- to the best of my knowledge and belief, or of the ordinary methods of desiccating food substances, the

results of which, as is well known, cause a stances, in subjecting it to a preliminary slight cooking process. 2d. In subjecting the material in masses of suitable size to they action of a current of air or equivalent gas in such a way as to give an equalized removal of the water without vinjuring the .cellular structure of the material, or cooking or otherwise chemically changing its composition in any other way than by removing thev water which is present, soto speak, mechanically, as moisture. The temperature Of the air mustv in any event not be high enough to give any chemical ehange in the succulent. food .material treated, as by breaking down compounds -in which Water exists in la state of combination; or be high enough to do more than merely remove moisture. Incidentally in some instances there may be a slight loss of ot-her ingredients, a loss too small to materially affect the product." 1

I have discovered by repeated experiments that, in order to obtain the desired results, the dehydration must be performed by a current of air or'other suitablegas, the initial temperature of which depends upon the kind of material being treated, this current being caused to thoroughly permeate the material by being forced to pass back and forth in alternating directionthrough successive portions of the saine, the entering undehydrated material first encountering air which has already passedV through pre: vious portions of the same or other material, and which is `therefore already charged with moisture, and, if initially heated, has

become more'or less`cooled. As the material progresses, it therefore encounters air which is more and more dry and of increasing or decreasing temperature until finally it comes in contact with air of the initial dryness and temperature which, as I have said, must be varied to suit the kind of material being treated. In this method of operation the amount of evaporation in a time unit is equalized, preventing sudden changes of.

composition.

I am aware that broadly considered the process just described, of subjecting the ma terial first to the action of air which has already absorbed moisture from the preceding material and gradually progressing the material until it comes in contact with air which has not as yet come in contact with any of the material, has been known-hith-- ing in any material Way the remaining solid substance. The dehydrated foods obtained by the present process are desiccated in such a manner as to lose only what is, so to speak,

the water mechanically present without los ing Water chemically present as water `of constitution orA the volatile oily bodies which give the aroma and taste to ordinary foods, andl such dehydrated foods therefore on rehydration by treatment with water reassume the condition of the original material. The results which I obtain by my process depend upon an additional feature, which lIbelieve to be absolutely new in this art,

and which I will now describe.

I have stated that the operation of dehyf drating vegetable and animalfood products mustbe conducted in amuch more gradual manner than the drying of pottery, etc., but it is not only necessary that the dryness and temperature of the air shouldbe gradually varied from the time the operation commenoes upon any given portion of material until it is completed thereupon in such manner as to equalize to some degree the amount of moisture evaporated in each stage of the drying, but I have determined that it is also necessary-and this I regard as an essential feature l/of lmy invention-to retard the flow of theair-as it leaves the apparatus in which' the material yis treated in such 'manner as to back it up as it were in the apparatus, thereby maintaining the air under a certain degree` of pressure while still permittingthe fiow of theflowing current of air, the amountofwhich varies with different 1naterials,=while at the same time 4permitting a gradual constant iow of air through the apparatus whereby the substances being treated areconstantly acted upon by fresh'air, which, being under pressure is forced to thoroughly permeate the pores and cells of the substances, and prevents -the crushing or rupturing of the cell walls as the dehydration progresses. There ymust be a flowing currentof air but this air must `be under some pressure. It is this ac tion, 4I believe, which maintains the substan-l tial composition of the materials unchanged and enables them to be restored by water to their original freshness. rllhe result of re-y tarding the egress of the air so as to set lup a certain pressure may be compared to that caused by placing a partial obstruction in a swiftly running stream. The water,- retarded in its flows rises and spreads, filling all the interstices 'and hollows among the rocks and in the banks, .which .previously were entirely passed byfor only partially filled by the fast-running water. This produces an even evaporative effect, greatly aiding in the even evaporation of the moisture in each individual particle; and -in order to produce products of the character contemplated in the present -invention, an even and progressive evaporative effect is necessary from first to last. lBut this is difficult to secure without special precautions since air in going through a permeable or pervious mass of matter is prone to flow mainly through particular channels. The reversal of the direction of flow of the air from time to time greatly aids in securing even evaporation since thereby opposite sides of any given granule or particle alternately become, soto speak, Windward and leeward sides. With the air always going one Way, one side of each article isl always a leeward surface and it is not exposed to the dehydrating effects of the air, to the same ext-ent as where the direction of the air is occasionally reversed. v The apparatus I employ in carrying out my process' may be of the type shown in my copending application for patent, filed.)r anuary 29, 1904, Serial No. 2191558 (Patent 867,246, Oct. 1, 1907), b ut it will be readily understood that the process may be carried out in different forms of apparatus, it being only essential that the subjection of the material to the action of the dry air be gradual, and that the egress of the air from the apparatus be retarded so as to cause the air to iio ` in the drawing.

vent any material change therein, other than the withdrawal of the water.-

As an illustration of a form of apparatus which may be employed in the carrying out of my process, I will refer to the accompanying drawing, in which- Figure l is a partial longitudinal, vertical section through a formof apparatus suitable for carrying out lny process. Fig. 2 is a horizontal section thereof on the line a-tz of Fig. 1.

In said figures 3, 3 represent the trays upon the perforated bottoms 4 of which layers of the material to be treated are placed, such material when necessary beingin a finely divided condition. These trays are movably supported on guide-ways 2, located ou the side-walls of the dehydrating chamber which is indicated as a whole by 10. The trays may slide on these guide-ways, as shown, or'be mounted on Wheels or^rol1 ers, as desired, and there may be guides above as well as below the trays, if desired.

The chamber 10 comprises a series of vsuperimposed tray compartments, avdescription of one of which will sutlice. The trays are inserted at 011e end of the compartment, the right hand end in Fig. 1, while the current of air lenters the ,left hand end of the compartment. The compartment is provided with partitions 5, extending alternately from the roof and floor thereof to said guideway 2, or into close proximity to the top and bottom of the trays. The' free ends of these partitions are provided with flexible packing strips 6 which'coact with the ends of the trays to form a practically air-tight joint. The distance be tween two adjacent partitions on the same side of the tray must be an exact multiple of the length of one tray, that is, it must be equal to the length of two or more trays, preferably to the length of two, as shown The traysare intermittently fed forward the length of one tray by pushing the last tray, either manually or by suitable mechanism, in until its rear end is in line with the end partitions 5, 5, which are arranged opposite each other, as shown, so as to prevent the egress of air. The other 'end of the compartment is provided with a glazed door 30, for the removal of the trays carrying the dehydrated material, and said door mayI conveniently be provided with a pair of cut-otts 32, one on each side, each having an aperture 33,.'Which coincide, when the door is "shut, with the passages 15, through which the dry air enters the. compartment. opened for the purpose of removing a tray, for example, said cut-offs closesaid passages and shut olf the air. Said passages 15 'com-l municate with air-mixing boxes 14,Which in turn communicate by passages 16 and 17 Thls, \When the door is` with air-ducts lland 12, into which maybe respectively cold and hot airfor'ced by va suitable blower (not shownlvthrou'ghpipes 13 and 14 leading from any suitable apparatus for drying, heating or cooling the air. The passagesl and 17' are provided with cutof valves 18, 18, whereby the qualities am! quantities of the air, 'aswell as thetemperature of the mixed current, admitted into the mixing-boxes 1t may be controlled at will. The ducts 11 and 12 are also provided with glazed doors 30, through which hygrometers 34 may be read, and the humidity of `thcair determined.

Peep-holes 7, normally closed by plugs, are provided in the side-walls of the chamber 10, through which the material being treated may be inspected at any time. At the other 4en'd of the chamber' 10 is located the air-egress chamber 2Q, communicating by passages 22 with each compartment thereof, valves 21 being provided to control said passages. In this way the pressure in each compartment may be regulated, pressure gages-38 being provided to indicate the same.' The air egress chamber 2() is also provided with a hygrometer 37 to indicate the humidity ofthe air leaving the chamber, and thermometers and 3G are located as shown to determine the temperatures of the air at the points indicated.

W'ith this apparatus it will, be obvious that as the trays are moved' forward the direction of the air flow through each tray is reversed from vtime to time. The arrangement of partitions shown gives a very -eonvenient way of securing this reversal since the Yair is caused to flow in a sinuous path through the drying chamber as a whole. alternately passing upward through a tray and downward through the next' tray, with a positive flow through each such tray. This arrangement has the advantage of not requiring special means to reverse the How of air 'from the air-supplying means from time to time. The successive trays filled with appropriate suitable permeable masses of succulent food material pass forward in a straight line, the air .is intlyluced at one end and emerges at the other; but the. advantages of alternate tiow arev automaticallir obtained and automatically as each tray passes-forward the 'leeward sides of the objects constituting the permeable mass of succulent food material in it become wind.-

The tray sides.

ward sides and vice versa. and partitions being imperforate and each tray relatively small, the l'feed of air through -the masses of succulent food material is positive; the same portion of air being .forced to pass through the material of each successive tray in the series.

Having thus described my invention. and aform of apparat-us which may be used to practise the same, what I claim and desire food substances without injurin to'secure byLetters Patent of the United States is:

.1. The process ot dehydrating succulent theircell strl'lcture ortexture, which conslsts in subjecting pervious masses of such substances to the dehydrating actionA of a flowing current ot air in moisture absorbing condition passed through such masses in a chamber maintained under pressure, vsaid air being at a temperature too low to produce chemical changes in said succulent oodsubstances and the air initially used in treating said substances containing some moisture,where by the Ywater. is removed from them with substantially no loss of other substances and they are left in a condition such that they can `be restored to' their original undehydrated condition simply by the addition of water;

2. The process of dehydrating succulent food `substances without injuring their cell structure, which consists in forcing a flowing current of air vin moisture absorbing condition .and of a temperature insufficient to produce chemical change in succulent food materials through permeable masses of' such material in a suitable chamber `and retard-ing the flow of the air from lsaid chamber so as to maintain the air in said chamber under pressure,lwhereby the water is removed-'from the material with substantially no loss of other substances and the -material is leftin a 'condition such that it can 'be restored to its original undehydrated condition simplyby the addition of water. 3. The process of dehydrating succulent food' substanceswithout injuringv their cell structure, which consists in dividing the material. into small pieces, and subjecting layers of the divided material to the dehydrating action of a flowing current of air passed therethrough in a chamber maintained -unde'r pressure,l said air vbeing in .moisture absorbing condition and'at a teme perature too -low t-o` produce cooking or other chemical changes in succulent food materlals, whereby the water is removed Vfrom the material with substantially no loss of other substances and the material is left in a condition. such that itvcan be restored to itsoriginal Vundehydrated condition simply bythe addition of water.

4. The process of -dehydrating succulent '.t'ood'substances without injuring their cell structure, which consists in slightly cooking the food substance, dividing 1t into small pieces, 'and' then subjecting layers of the divided material Vin a chamber maintained under pressure to the .dehydrating action of a currei'it of air passed'therethrough and at a temperature too low to produce any further coo-king or. other. chemical changes in said succulent food materials, whereby the water is removed from the material with substantially no loss of other substances and the material is left in a condition such that it can be restored to its original undehydrated condition simply by the addition of Water..

5. The process of dehydrating succulent food substances without injuring their cell structure, which consists in subjecting permeable masses of the material to be dehydrated in a chamber maintained under presthat it can be restored to its original lindehydrated condition simply by the addition of water.

6. The process of dehydrating succulent food substances without injuring their cell structure, which consists in subjecting permeable masses of the material tobe dehydrated in a chamber maintained under pressure to the dehydrating action of a flowing -current of air passed therethrough and containing some moisture and in then subject-- ing the partially'dried material while stili underpressure to the action of a flowing current of air at a higher telnperature and containing less moisture than the air used at the beginning of the treatment, whereby water is'removed from the material with substantially no loss of other substances and 'such material is left in a condition such that it can be restored to its original undehydratedcondition simply by the addition of water.

7. The process of dehydrat-ing succulent food materials which comprises placing a permeable mass of such material in a suitableholder and subjecting the mass while in a chamber maintained under pressure to the passage of a owing current of air until the desired degree 'of Idehydration is completed, thepassage of said current of air therethrough being reversed in direction at 'short intervals and theair initially passed 9. In the dehydration of succulent food I materials, the process which comprises passing ya current of a gaseous dehydrating agent through a permeable mass of such a material, the direction of passage of said current through said mass being reversed from time to time at short intervals to cause opposite sides of saidmass to become alternately leeward and Windward sides. X

10. In the dehydration of succulent food materials, the process which comprises passing a current of air through a permeable mass of such a material, the direction ot' passage of said current through said mass being reversed from time to time at short intervals to cause opposite sides of said mass to become alternately leeward and Windward sides.

11. In t-he dehydration of succulent food materials, the process which comprises establishing a continuously iowing current of air, and transmitting acontinuous succession of permeable layers of such a material'across the path of said current in such manner that said current enters each successive layer at a different face.

12. In the dehydration' of succulent food materials, the process 'which comprises establishing a current of air. continuously flowing in a sinuous line in a given direction and passing a succession of permeable layers of such a material in the opposite direction in such a manner that said current asses through each successive layer in a di 'erent directlon.

13. In the dehydration of succulent vegetable materials, the process which comprises passing a current of air through a permeable mass of such a material in a suitable chamber maintained under pressure, the direction of passage of said current through said mass being reversed from time to time to cause opposite sides of said mass to become alternately leeward and Windward sides.

14. In the dehydration of succulent vegetable materials, the process which comprises passing a succession of trays containing perlneable layers of such a material through a comparatively long tunnel-like chamber, and passing a current of air through said tunnel-likechamber in the opposed direction and causing such air current to travel. in a sinuous path -through said chamber, cnter ing and passing through successive trays in ditlerent directions.

In testimony whereof, I aiiix my signature, in presence of two witnesses.

ERNEST WILLIAM COOKE.

Witnesses:

GEO. W. JAMES, JOHN S. POTTER. 

